Research on the effects of liquid viscosity on droplet size in vertical gas–liquid annular flows
Authors:
- Zhiyuan WangZWZhiyuan Wang
- Hui LiuHLHui Liu
- Zhennan ZhangZZZhennan Zhang
- Baojiang SunBSBaojiang Sun
- Jianbo ZhangJZJianbo Zhang
- Wenqiang LouWLWenqiang Lou
- 1 July 2020
- journal article
- research article
- Published by Elsevier in Chemical Engineering Science
- Vol. 220
Abstract
No abstract availableFunding Information
- Ministry of Industry and Information Technology of the People's Republic of China
- China National Petroleum Corporation
- National Natural Science Foundation of China
- Natural Science Foundation of Shandong Province
This publication has 42 references indexed in Scilit:
- On the modelling of droplet–film interaction considering entrainment, deposition and breakage processesChemical Engineering Science, 2009
- Droplet size measurements in horizontal annular gas–liquid flowInternational Journal of Multiphase Flow, 2001
- Detailed Measurements of Vertical Annular Two-Phase Flow—Part I: Drop Velocities and SizesJournal of Fluids Engineering, 1994
- Maximum and mean droplet sizes in annular two-phase flowInternational Journal of Heat and Mass Transfer, 1994
- Analytical and Experimental Investigation of Entrainment in Capillary Pumped Wicking StructuresJournal of Energy Resources Technology, 1993
- The effect of gas properties on drops in annular flowInternational Journal of Multiphase Flow, 1989
- Modelling flow pattern transitions for steady upward gas‐liquid flow in vertical tubesAIChE Journal, 1980
- Entrainment Rate and Size of Entrained Droplets in Annular Two-Phase FlowBulletin of JSME, 1979
- Stability of droplets suddently exposed to a high velocity gas streamAIChE Journal, 1964
- Fundamentals of the hydrodynamic mechanism of splitting in dispersion processesAIChE Journal, 1955